ADHESION PROMOTERS

Abstract: The invention relates to polyamide resins which may be used as, among other things, adhesion promoters for polymers and copolymers, in particular for polymers and copolymers of vinyl chloride. These resins are prepared by reacting amines with carboxylic acids in a multi-step process in which, in a first step, polyvalent carboxylic acids are reacted with a stoichiometric deficiency of polyamines in the presence of an organic solvent which forms an azeotrope with water, water being removed. The reaction is controlled by means of the amount of water formed and removed during the condensation and, possibly, during the imidazoline formation. After removal of the theoretical amount of water or a lesser amount, in a further step more amine is added to the reaction mixture in an amount sufficient to achieve a final amine number of 10 to 300 mgKOH/g, the reaction is continued, the residual water is completely removed, and the remaining solvent is completely or partially removed.

Description: ADHESION PROMOTERS The invention relates to polyamide resins based on organic acids, e.g., mixtures of mono eric, dimeric, and tri eric fatty acids, and amines, which can be used for, among other things, as adhesion promoters for polymers and copolymers, more particularly for polymers and copolymers of vinyl chloride, to a process for preparing such resins, and to their use as adhesion promoters. Polyamide resins of the aforementioned type have long been known. For 10 instance, Ullmann's Encyklopadie der technischen Chemie, 3rd Ed. (Mϋnchen-Berlin: Urban & Schwarzenberg Verlag, 1963) in Vol. 14, pp. 73-75 describes polyamide resins which are prepared from amines such as ethylene diamine and other polyethylene amines and branched dicarboxylic acids made from unsaturated fatty acids. The use of 15 trimeric fatty acids and monomeric or trimeric carboxylic acids for the composition of such polyamide resins is also mentioned. Mentioned as fields of application for these polyamides, which are of a waxy or resinous character, are, among other applications, the 20 curing of epoxide resins, the bonding of raw materials, the manufacture of composite component parts, and the like. Polyamide resins find a further field of application as adhesion promoters, especially in so-called plastisols. These are liquid to 2 c pasty dispersions of a powdery polymerisate in a plasticiser. Plastisols are used, for example, for heat- and sound-insulating layers, for protection against corrosion and stoning (damage caused to coated bodies by stones or pebbles impacting on their surface), which , n in this case are principally applied in the construction of automobiles by means of application onto various kinds of metal surfaces. While plastisols can display certain adhesive properties, these do not always comply with the today's high requirements. For there is insufficient adhesion in certain places after application of the protective layer or if the adhesion loosens in due course, corrosion may set in very rapidly. Also in the case of mechanical stress the protective layer may come off. So far, there has been no lack of attempts to improve the various polyamide resins in order to adapt them for certain applications. The objective of this development work has been the improvement of polyamide resins for their use as adhesion improvers or adhesion promoters, with regard to their adhesive properties, processability, intake of water, storage stability, and their resistance to high temperatures, light, and radiation. This has already been attempted and accordingly, German Patent Specification 3 111815 describes the improvement of the adhesive properties of plastisols by condensing 0 to 0.5 equivalents of certain polycarboxylic acids originating from the polymerisation of unsaturated fatty acids and 0.5 to 1 equivalents of dicarboxylic acids such as adipic acid with 1 to 2 equivalents of particular aliphatic polyamines. However, the thermal stability of these plastisols still leaves something to be desired. European Patent Application 171 850 describes the improvement of the thermal stability of a plastisol by the addition of polyamide resins based on the condensation of 1.0 to 2.2 equivalents of an heterocyclic polyamine such as piperazine or N-aminoethyl piperazine with a polycarboxylic acid. The process described in this application is difficult to control and frequently leads to very high molecular weight polymers which are not suitable for further processing. It is also often impossible to bring the condensation to a conclusion because the viscosity increases so rapidly during the reaction that the mixture is no longer stirrable leading to premature stoppage of the reaction. The process described in European Patent Application 378205 behaves in the same way. A further drawback to the above-mentioned processes is that the improvements always go more or less in one direction, and that, for instance, the improvement in thermal stability is achieved at the expense of a deterioration of the processability. Although numerous processes are already known which describe the manufacture of polyamide resins which can also be used as adhesion promoters, there is still a need for improved processes yielding products with enhanced properties which can be applied in various fields of application. Consequently the object of the invention is to provide a process which is easy to carry out, can be controlled properly and yields reproducible products which display favourable properties of adhesion, resistance to the action of heat and light and a low intake of water. The invention also has the objective of providing a process which permits the selective adjustment of one or more specific properties, thus enabling the manufacture of custom-made products for varied application purposes and processing conditions. Additional advantages of the invention follow in the remaining description and examples. The objective is reached by a process for the preparation of polyamide resins having an amine number of 10 to 300 mgKOH/g. The process entails the reaction of amines with carboxylic acids in a multi-step process, characterized by, in a process with at least two-steps, a first step where polyvalent carboxylic acids, optionally together with monovalent carboxylic acids, are reacted with a stoichiometric deficiency of polyamides. The reaction is carried out in the presence of an organic solvent which can form an azeotrope with water and is therefore used to remove the reaction water. The reaction is controlled by means of the amount of water collected from the condensation, and possibly from the formation of i idazoline. After removal of the theoretical or a lesser amount of water, in a second step an amount of amine sufficient to achieve a final amine number of 10 to 300 mgKOH/g is added to the reaction mixture. The reaction is continued until no more water can be collected. After which time the residual water is removed with all or some part of the solvent. Preferably the amines are used in an amount leading to a final amine number of 100 to 160 mgKOH/g. It is especially advantageous to add the amines in such an amount that in the final step all the carboxylic acid groups will have been reacted. In the first step, preference is given to use of a single amine. It is advantageous when, after the first step and prior to the further step, an additional amine is added in a second step. The reaction is continued in a similar way to the first step, removing the water produced. Preferably, in the first step a mixture of dimeric and trimeric carboxylic fatty acids is used, optionally containing some monomeric carboxylic fatty acid and/or dicarboxylic acid. Especially suitable for the first step are one or more amines such as polyalkylene amines, more particularly polyethylene amines of the H(NH-CH2CH2) X -NH2 type. Instead of the ethylene radical there may be another divalent aliphatic, cycloaliphatic, aromatic, arylaliphatic, heterocyclic, or hetero-atom interrupted aliphatic radical. Each hydrogen atom on the terminal amino groups may be replaced with corresponding substituents, e.g., of an aliphatic nature. Also highly suitable as amine for the first step are piperazines, N- aminoethyl piperazine, and amines derived from piperazines of the following formulae: H-N N-CH 2 -CH 2 -N N-CH -CHp-NH?, (I) H N-CH -CH2-N -CH2-CH2-NH2, (II) H-N -CH2-CH2-NH2, and (III) 0 = 1 - 8 H2N-CH2-CH2-N N-CH2-CH2-NH-CH2-CH2-NH-CH2-CH2-NH2. (iv) The following polyamines, without restriction or limitation, are particularly suitable for use in the first step: 1,2-ethane diamine; 1,3-propane diamine; 1,2-propane diamine; 1,3-pentane diamine; 3-azapentane-l , 5-di ami ne ; 3,6-diazaoctane-l,8-diamine; 3,6,9-triazaundecane-l,ll-diamine; 3,6,9,12-tetradecane-l,14-diamine; 3-azahexane-l , 6-di ami ne ; 4-azaheptane-l,7-di amine; 4, 7-di azadecane-1 , 10-di ami ne; 3-amino-l-methyl aminopropane; 3-amino-l-cyclohexyl aminopropane; neopentane diamine; 1,6-hexane diamine; 1,8-octane diamine; 2,2,4-trimethyl hexamethylene diamine; 2,4,4-trimethyl hexamethylene diamine; 4,9-dioxadodecane-l,12-diamine; 4,7, 10-tri oxatri decane-1 , 13-di ami ne; 4, 4 '-di ami nodi cycl ohexyl methane; 3, 3 ' -dimethyl -4, 4 '-di ami nodi cycl ohexyl methane; 3-aminomethyl-3,5,5-trimethyl cyclohexyl amine; 1,2-di ami nocycl ohexane; 1,3-bis (amine methyl ) cycl ohexane; 4,4'-diaminodiphenyl methane; m-phenylene diamine; di ethyl toluene diamine; -xylylene diamine; Jef famine® D-230; Jef famine ® D-400; Jef famine® D-2000; Jef famine® ED 600; Jef famine® ED-900 and; Jef famine® T-403. The following compounds, without restriction or limitation, are considered suitable monoamines for the further step, i.e., the final step: dimethyl aminopropyl amine; Duo een ® CD (R-NH-CH 2 -CH2-NH 2 ) ; Armeen® (ex. AKZO Chemicals fatty amines); hexyl amine; octyl amine; dibutyl amine; di-2-methoxyethyl amine; 3-ethoxy-l-propane amine; cyclohexyl amine; Jeffamines ® are commercial products of Texaco Chemical Company. In the further and/or, optional, second step, use is advantageously made of di- or polyfunctional amines having amine functions of varying reactivity. For the second and/or third step monoamines may be used or co-used. In a particularly favourable embodiment of the process according to the invention a plasticiser is added during the further (final) step following the removal of the residual water. Especially suitable as plasticisers for this purpose are benzyl alcohol, dioctyl phthalate, diisopropyl phthalate, dibutyl ether, diisopropyl naphthalene, and mixtures thereof. Especially suitable as solvents forming an azeotrope with water are, according to the invention, toluene and/or xylene as well as dibutyl ether. Further embodiments of the invention are constituted by polyamide resins which can be obtained according to any one of the aforementioned processes, and their use as adhesion promoters. The process according to the invention may be carried out as indicated below. The polyvalent carboxylic acids to be condensed, and which may be obtained from, for example, polymerisation of unsaturated fatty acids, are dissolved or dispersed in a solvent forming an azeotrope with water. These carboxylic acids are composed primarily of di ers and trimers which can be obtained via the polymerisation of unsaturated fatty acids. In addition, monomeric fatty acids may be present in the mixture. It is also possible to add saturated monocarboxylic acids as well as dicarboxylic acids not obtained via the polymerisation of fatty acids, e.g., adipic acid. The carboxylic acids which may be employed are mainly commercially available products. The preferred carboxylic acids and the so-called polymerised fatty acids which are obtained from unsaturated fatty acids. Further details regarding such acids can be found in, for example, EP-A-0084 111, notably on pages 6 and 7, which disclosure is specifically referred to here. Polyamines are then added in stoichiometric deficiency to a solution or dispersion of the polymerized fatty acids. By stoichiometric deficiency is meant that per equivalent of carboxyl groups of the acids, less than one equivalent of reactive amine groups is added. Favourable ratios are, for example, 0.3 to 0.8 equivalents of reactive amine groups per equivalent of carboxyl groups. Reactive amine groups are those amine groups which are able to condense or polycondense with carboxyl groups. For diamines such as ethylene diamine or piperazine these are the two primary or, alternatively the secondary amine groups. In the case of polyamines containing more than two amine groups such as polyethylene polyamines, e.g., diethylene triamine, triethylene tetramine, only the two primary amine groups are considered to be reactive amine groups. In the first step, the "backbone" of the polyamide resin is formed. This building up of the backbone may be continued in the steps preceding the last (further) step, if desired. Preferably, diamines are employed in the first step. Although it is possible to use diamines having varying amine functionalities, such as N-aminoethyl piperazine, amines with two equivalent amine functionalities are the most suitable for the first step, in particular those amines of the formulae I and/or II. The appropriate amines are without exception, commercially available products. Examples of amines which may be used within the framework of the invention are to be found in, for example, EP-A-0098372, more particularly on pages 6 and 7, which disclosure is specifically referred to here. Also suitable are the Jeffamines ® . By selecting the acids, the ratio of dimers and trimers and optional monomers, when present, and the amine, it is possible according to the invention to build up a polyamide resin backbone having a wide range of tailored properties. Thus, the adhesion properties may be varied via the proportion of trimeric acids, while the use of piperazine or N-aminoethylpiperazine will influence the thermal stability. The reaction is carried out at elevated reaction temperature, which will be generally at a level of at least 120°C. The required temperature can be influenced by the use of a solvent, the reactant concentration, and the pressure. If a certain amount of imidazoline formation is required, the temperature must be raised since, generally, imidazoline formation takes place at higher temperatures than amide formation. The water which forms during the reaction is removed by means of azeotropic distillation. The amount of outgoing water is measured and more amine is added in a further step when the desired amount of water has been separated. This may be the theoretical amount corresponding to, for example, 0.8 equivalents of reactive groups employed, or, alternatively, a lesser amount. The desired amount of water to be removed can be calculated in advance and corresponds to the amount of water which is released by the condensation of the amine and the carboxyl groups to form the amide groups and, when required, from the formation of imidazoline. Advantageously, in the further step and, when desirable, in the intervening second step, amines are introduced which are comprised completely or in part of amines having amine functions of varying reactivity, e.g., N-aminoethyl piperazine. Alternatively, at this stage it is possible to use monoamines or polyamines, such as dimethyl aminopropyl amine, which having only one primary amine group and a tertiary amine group will behave like a monoamine. The further, i.e., final step, which is the second step in a two-step process, or the third step in a three-step process, etc., serves to continue and conclude the condensation process and, above all, to determine the final amine number which is of major importance to the goal of the application. It also plays an important role in the use of polyamide resin as an adhesion promoter by influencing the processability and thermal stability of the compound, which, besides the polymer such as PVC, and the plasticiser, also contains various other ingredients, such as pigments, calcium carbonate, additives, etc. The final step also serves to react, quantitatively if possible, the remaining carboxyl groups. Preferably, the entire amount of the amines used in the various steps is so chosen as to give precisely enough amine groups to react all the carboxyl groups in the reaction mixture which are derived from carboxylic acids. In the preparation of polyamide resins according to the invention, which resins are intended to be used as adhesion promoters in plastisols, it is above all of advantage to add a plasticiser in the further (final) step after removal of the residual water and partial or complete removal of the solvent. This facilitates the further processing of the adhesion promoter in the plastisols. If desired, there may be added in addition to, or instead of, plasticisers, other substances which may be relevant to the further processing of the material, e.g., white spirit. Although here mention is generally made of two steps, i.e., the first and the further step, or of three steps, i.e., the first, the second, and the further step, it is also possible according to the invention to carry out the preparative process in more than three steps. For instance, the first step can also be carried out in several sub-steps, and the same goes for the other steps. It is particularly surprising that the process according to the invention permits the selective preparation of polyamide resins having a wide range of uses and possessing excellent properties. The preparative process is readily controllable and the highly undesirable gel formation, which occurs when the condensation gets out of control and which leads to useless waste, does not arise. Properties such as viscosity and processability can be carefully regulated, as can the chemical composition, so that polyamide resins having a particular property profile can be selectively prepared. In practice, it has been shown to be scarcely possible to prepare a "universal" adhesion promoter. Thus, for instance, in the automobile industry the type of sheet metal used, the type of dip coating, etc. have an effect on the serviceability of a compound whose properties and processability will be greatly affected by the adhesion promoter. The process according to the invention offers a method which permits a flexible approach to even the most varied customer wishes and to successful optimization of property profiles. Furthermore, the polyamide resins according to the invention may be employed as curing agents for epoxide resins and isocyanates, as well as in fields where polyamide resins are commonly used. The invention will be further illustrated with reference to the following examples. Example 1: Preparation of a polyamide resin which may be used as an adhesion promoter for plastisols, in a two-step process, Acid/lst amine/2nd amine equivalency ratio = 21/12/9. Into a 700 ml glass reactor equipped with a corresponding flanged head, an electrically driven stirrer, a thermometer, and a Dean-Stark water trap were charged 171 g of Pripol 1040 (0,6 equivalents). Pripol is a polymerised fatty acid essentially composed of about 80% of trimers and about 20% of dimers. Also 150 g of xylene were added. The mixture was stirred and simultaneously heated to 100°C. Within 5 minutes 14,8 g of piperazine (0,344 equivalents) were added, with the temperature rising to about 112°C. After that, the temperature was raised until refluxing started and the reaction continued until 6,2 g (0,344 equivalents) of water had been removed; about 6 hours were needed to accomplish this. The mixture was then cooled to 120°C, and within 10 minutes 33,2 g (0,2574 equivalents) of N-aminoethyl piperazine were added. The mixture was again heated until refluxing started and the reaction continued until 4,5 g (0,2500 equivalents) of water had been removed (the theoretical value was 4,6 g) . After that, the mixture was cooled to 120°C. The Dean-Stark water trap was replaced by a distillation head, the pressure was reduced to 20 mbar, and xylene and the residual amount of water were removed, in which process a maximum temperature of about 160° to 170°C was reached in the reactor. When there was no longer any distillate being distilled, the mixture was cooled to 120°C under vacuum prior to being subjected to standard pressure again. After that, 208,6 g of diisopropyl naphthalene were added in order to reduce the viscosity and improve the processability. Obtained were 417 g of a deep-brown liquid. Analysis of this product produced the following values: amine number: 82 mg KOH/g (perchloric acid method) viscosity at 20°C: 89,4 Pa.s Pripol 1040 is a commercial product ex Unichema Chemie GmbH, D 4240 Emmerich. Examples 2 to 8: In the same manner Pripol 1040 was reacted with different amines in a two-step process. The further details can be taken from Table I. co r*o r o «-" ° Tabl e I Exampl e 2 3 4 5 6 7 8 equivalency ratio 12/6/6 12/6/6 12/6/6 12/6/6 21/12/9 42/26/16 12/6/6 Pripol 1040 (g) 171.0 171.0 171.0 171.0 171.0 171.0 171.0 1. amine TETA - 22.5 - TEPA - - 33.0 - N-AEP 19.4 - - 19.4 - - 19.4 PIP - 14.8 16.0 separated water (theor.) 5.1(5.4) 5.7(5.4) 5.5(5.4) 5.2(5.4) 6.0(6.2) 6.6(6.7) 5.2(5.4) 2. amine N-AEP 38.8 38.8 38.8 38.8 AEEA - 26.8 - 31.2 DMAPA - - - - 24.5 separated water (theor.) 5.1(5.4) 8.1(5.4) 9.6(5.4) 5.1(5.4) 8.4(4.6) 4.1(4.3) 8.2(5.4) plasticiser diisopropyl naphthalene - 218.5 227.7 218.9 100.0 100.0 100.0 benzyl alcohol - 98.2 100.8 108.2 di-octyl phthalate 219.0 - - amine no. (mg KOH/g) 99 119 136 101 53 57 68 viscosity at 20°C (Pa.s) 32.8 37.2 8.6 4.3 7.5 active product 50 50 50 50 50 50 50 Example 9: Preparation of a polyamide resin which may be used as an adhesion promoter for plastisols, in a 3-step process. Acid/lst amine/2nd amine/3rd amine equivalency ratio = 21/12/4/5. Into a 700 ml glass reactor equipped in the same manner as that employed in Example 1 were charged 171,0 g (0,6 equivalents) of Pripol 1040. Also added were 150 g of xylene, and the whole was mixed through stirring and heated to 100°C. Within 5 minutes 25,7 g (0,345 equivalents) of TETA were added, with the temperature rising to 113,6°C. After that, the temperature was raised until refluxing started (139° to 141°C) . The reaction was continued until 6,4 g of water had been removed. This took about 40 minutes. The mixture was then cooled to 120°C. Within 10 minutes 30,9 g (0,114 equivalents) of Duomeen CD (a fatty amine produced by Akzo Chemicals GmbH, Dϋren) were added. The mixture was again heated until refluxing started (152° to 154°C) . It was then kept under reflux for 6 hours, until 2,1 g of water had been removed. The mixture was then cooled to 120°C. After that, 18,4 g (0,143 equivalents) of N-aminoethyl piperazine were added within 10 minutes. The reaction was continued until all of the water had been removed. This final step required about 4 hours, with 6,5 g of water being removed in the process. The increased amount as compared with the theoretical value (2,6 g) has its origins in the imidazoline formation. After that, the mixture was cooled to 120°C. Xylene and residual water were removed in the same manner as in Example 1. 231,2 g of diisopropyl naphthalene were added in order to improve the viscosity and the processability. Obtained were 462 g of a deep-red product. The product had the following properties: amine number: 97 mg KOH/g (perchloric acid method) viscosity at 20°C: 33,1 Pa.s Examples 10 to 15: In the same manner Pripol 1040 was reacted with different amines in a 3-step process. The further details can be taken from Table II. co ι * *o ι*o o n o Table II Example ~ Tθ ~ 11 12 13 14 15 equivalency ratio 21/12/7/2 12/4//2/6 12/4/6 12/4//2/6 12/2/4/6 12/4/2/6 Pripol 1040 (g) 171.0 171.0 171.0 171.0 171.0 171.0 solvent xylene toluene xylene xylene xylene xylene 1. amine PIP 14.8 8.9 8.9 8.9 8.9 TETA 15 separated water (theor.) 6.1(6.2) 3.7(3.6) 3.5(3.7) 3.5(3.7) 3.5(3.7) 3.5(3.7) 2. amine AEEA 20.8 - - PIP 4.3 Jeffamine D-400 20.0 Jeffamine ED-900 49.0 TETA 7.5 separated water (theor.) 4.4(3.6) 1.8(1.8) 1.6(1.8) 1.7(1.9) 3.1(1.8) 1.7(1.8) 3. amine N-AEP 7.8 38.7 38.7 38.7 - 38.7 Duo een CD 84.0 separated water (theor.) 3.2 ( 1.1) 5.7 (5.4) 5.0(5.4) 5.5 (5.4) 5.4 (5.4) 5.4 (5.4) plasticiser diisopropyl 200.7 216.4 228.5 256.9 259.4 219.5 naphthalene amine no. (mg KOH/g) 60 103 72 63 63 88 vi scosi ty at 20°C (Pa . s) 13.3 112 27.3 17.6 5.1 24.3 acti ve product 50 50 50 50 50 50 Examples 16 to 17: In the same manner as described in Example 1 Pripol ® 1017 (about 80% of dimer and 20% of trimer) was used instead of Pripol ® 1040. Further details can be taken from Table III. T a b l e III Example Ϊ6 Ϊ7 equivalency ratio 20/18/2 20/18/2 Pripol 1017 (g) 171.0 171.0 1. amine TETA 40.5 PEHA 72.6 separated water (theor.) 9.5(9.7) 10.1(9.7) 2. amine N-AEP 1.1 7.7 separated water (theor.) 6.2(1.1) 5.3(1.1) plasticiser diisopropyl naphthalene 203.5 235.9 result amine no. (mg KOH/g) at 20°C (Pa.s) 94.7 156 viscosity at 20°C (Pa.s) 32 85 active product 50 50 % imidazoline ca. 53 ca. 53 Explanation of the abbreviations used in the examples: Jef famine D-400 polyoxypropylene diamine with an average molecular weight of 400 N-AEP N-aminoethyl piperazine DETA di ethyl ene tri amine TETA triethylene tetramine TEPA tetraethylene pentamine PEHA pentaethylene hexamine NN-DAPP 1,4-bis(3-aminopropyl)piperazine Amine N4 linear polyamine ex BASF DMAPA dimethyl aminopropyl amine P-101 phenyl glycidyl ether/DETA adduct product of Akzo Chemicals GmbH Dϋren Laromine C252 product of BASF - cycloaliphatic diamine Duomeen CD AKZO product - fatty polyamine RV 1805 product of Ems Chemie o-cresyl glycidyl ether GE glycidyl ether KMC non-reactive diluent DOP di-octyl phthalate BZA benzyl alcohol

Claims: Claims 1. A process for the preparation of polyamide resins having an amine number of 10 to 300 mgKOH/g by reacting amines with carboxylic acids in a multi-step process, characterised in that, in an at least two-step process, in the first step polyvalent carboxylic acids, optionally together with monovalent carboxylic acids, are reacted with a stoichiometric deficiency of polyamines in the presence of an organic solvent which forms an azeotrope with water, water is distilled off, and the reaction is controlled by means of the amount of water formed by the condensation and, optionally, by the imidazoline formation, and, after removal of the theoretical amount of water or a lesser amount; in a further step more amine is added to the reaction mixture in an amount sufficient to achieve a final amine number of 10 to 300 mgKOH/g, the reaction is continued, substantially all of the residual water is removed, and the residual solvent is completely or partially removed. 2. A process according to claim 1, characterised in that the amount of amines used is such that the amine number is 100 to 160 mgKOH/g. 3. A process according to claim 1 or 2, characterised in that the amount of amines used is such that in the final step all of the carboxyl groups will have been reacted. 4. A process according to one or more of claims 1 to 3, characterised in that in the first step use is made of a single polyamine. 5. A process according to one or more of claims 1 to 4, characterised in that, after the first step and prior to the further step, more amine is added in a second step and the reaction is continued in a manner similar to that of the first step and water is removed. A process according to one or more of claims 1 to 5, characterised in that in the first step use is made of a mixture of dimeric and trimeric fatty acids, which, optionally, also contains monomeric fatty acids and/or dicarboxylic acids. A process according to one or more of claims 1 to 6, characterised in that in the further and/or optionally also in the second step use is made of di- or polyfunctional amines having amine functions of varying reactivity. A process according to one or more of claims 1 to 7, characterised in that in the second and/or the further step use is made of monoamines. A process according to one or more of claims 1 to 8, characterised in that in the further step a plasticiser is added. 10. A process according to claim 9, characterised in that the plasticiser used is benzyl alcohol, dioctyl phthalate or diisopropyl naphthalene, or a mixture thereof. 11. A process according to one or more of claims 1 to 10, characterised in that the solvent used to form an azeotrope with water is toluene and/or xylene. 12. Polyamide resins obtainable by a process according to any one of claims 1 to 11. 13. Use of the polyamide resins according to claim 12 as adhesion promoters.

Inventors: RAYMOND WILLIAM RENE EDUARD, RAYMOND, WILLIAM, RENE, EDUARD
Applicants: AKZO NOBEL NV, RAYMOND WILLIAM RENE EDUARD, AKZO NOBEL N.V., RAYMOND, WILLIAM, RENE, EDUARD
Application year: 1994
Main classification: C08G69
IPC codes: C08G69, C09J177